Process and device for cement clinker production

Patent metadata

Field	Value
Publication number	US-10106459-B2
Application number	US-201414784331-A
Country	US
Kind code	B2
Filing date	Apr 8, 2014
Priority date	Apr 15, 2013
Publication date	Oct 23, 2018
Grant date	Oct 23, 2018

Abstract

In a process for the production of cement clinker, in which raw meal is preheated in a preheater ( 3 ) using the hot exhaust gases from a clinker kiln, and the preheated raw meal, which is optionally calcined in a calciner ( 4 ), is burned to clinker in the clinker kiln ( 2 ), wherein the preheater ( 3 ) comprises at least one string of a plurality of cyclone suspension-type heat exchangers ( 8, 9, 10 ), through which the kiln exhaust gas successively flows and in which the raw meal is preheated in stages, a partial stream of the kiln exhaust gas is diverted such that only a remaining residual stream of the kiln exhaust gas is utilized for preheating the raw meal.

First claim

The invention claimed is:

1. A process for the production of cement clinker comprising:
preheating raw meal in a preheater using hot clinker kiln exhaust gas from a clinker kiln, wherein the preheater comprises at least one string of a plurality of cyclone suspension heat exchangers through which the hot clinker kiln exhaust gas successively flow and in which the raw meal is preheated in stages, and wherein the string of a plurality of cyclone suspension heat exchangers includes a first cyclone suspension heat exchanger and a last cyclone suspension heat exchanger,
burning the preheated raw meal, which is optionally calcined in a calciner, to clinker in the clinker kiln,
diverting a partial stream of the hot clinker kiln exhaust gas such that a remaining residual stream of the hot clinker kiln exhaust gas is utilized for preheating the raw meal,
drawing off hot clinker kiln exhaust gas from the last cyclone suspension heat exchanger in the at least one string of the plurality of cyclone suspension heat exchangers, and
mixing the diverted partial stream of the clinker kiln exhaust gas with the clinker kiln exhaust gas drawn off the last cyclone suspension heat exchanger, viewed in the flow direction of the clinker kiln exhaust gas.

2. A process according to claim 1 , wherein said process further comprises diverting the partial stream of the clinker kiln exhaust gas after the first cyclone suspension heat exchanger, viewed in the flow direction of the kiln exhaust gas.

3. A process according to claim 2 , wherein the at least one string of a plurality of cyclone suspension heat exchangers further comprises a second cyclone suspension heat exchanger and the partial stream of the clinker kiln exhaust gas is diverted so as to flow between the first and the second cyclone suspension heat exchangers, viewed in the flow direction of the kiln exhaust gas.

4. A process according to claim 1 , wherein the mixing is at a volume ratio of the diverted partial stream and the remaining residual stream of the clinker kiln exhaust gas is of 1:99 to 40:60.

5. A process according to claim 1 , wherein the process further comprises directly feeding the diverted partial stream of the clinker kiln exhaust gas and the clinker kiln exhaust gas drawn off the last cyclone suspension heat exchanger, viewed in the flow direction of the kiln exhaust gas, to a mixing device for mixing.

6. A process according to claim 5 , wherein the process further comprises mixing the diverted partial stream of the clinker kiln exhaust gas and the clinker kiln exhaust gas drawn off the last cyclone suspension heat exchanger in a mixing ratio selected such that the hot gas leaving the mixing device has a temperature of 400° C. to 550° C.

7. A process according to claim 1 , wherein the process further comprises utilizing sensible heat of the diverted partial stream, and optionally of the residual stream of the clinker kiln exhaust gas from the last cyclone separation heat exchanger.

8. A process according to claim 7 , wherein the utilizing further comprises drying raw material and/or drying fuel, and the process further comprises feeding the dried raw material to the preheater and/or using the dried fuel in calcining or in the burning in the process for the production of cement clinker.

9. A process according to claim 7 , wherein the utilizing comprises using the sensible heat in a heat recovery boiler to generate steam.

10. A process according to claim 7 , wherein the utilization excludes the use in a drying unit for drying wet waste substances containing organic components, whose drier exhaust gases are fed the calciner.

11. A process for the production of cement clinker comprising:
preheating raw meal in a preheater with exhaust gas from a clinker kiln, wherein the preheater comprises at least one string of cyclone suspension heat exchangers comprising a first cyclone suspension heat exchanger, at least one intermediate cyclone suspension heat exchanger, and a last cyclone suspension heat exchanger in series, whereby the raw meal is preheated in stages;
optionally calcining the preheated raw meal;
feeding the preheated, and optionally calcined, raw meal to a clinker kiln, burning the preheated raw meal in the clinker kiln and generating clinker kiln exhaust gas;
drawing the clinker kiln exhaust gas, optionally initially through the calciner, through the first cyclone suspension heat exchanger;
separating the clinker kiln exhaust gases from the first cyclone separation heater into a diverted partial stream of clinker kiln exhaust gases and a residual portion of clinker kiln exhaust gas;
drawing the residual portion clinker kiln exhaust gas successively and counter-currently through the remaining cyclone suspension heat exchangers in the at least one string of cyclone suspension heat exchangers,
drawing off residual clinker kiln exhaust gas flowing from the last cyclone suspension heat exchanger, and
mixing the diverted partial stream of the clinker kiln exhaust gas with the residual portion clinker kiln exhaust gas drawn off from the last cyclone suspension heat exchanger to obtain a gas mixture.

12. The process according to claim 11 , wherein said process further comprises calcining a portion of preheated raw meal to obtain a calcined product and feeding the calcined product to the clinker kiln.

13. The process according to claim 12 , wherein said process further comprises feeding a portion of uncalcined preheated raw meal to the clinker kiln.

14. The process according to claim 11 , wherein said process further comprises feeding uncalcined preheated raw meal to the clinker kiln.

15. The process according to claim 11 , wherein the process further comprises drying raw meal with the gas mixture, and feeding the dried raw meal to the preheater.

16. The process according to claim 11 , wherein the clinker kiln further comprises a firing system that uses fuel, and the process further comprises drying fuel, and using the dried fuel as fuel in the firing system.

Assignees

• Holcim Technology Ltd

Inventors

• Gasser Urs

Classifications

• C04B7/475 Primary

  using the waste heat, e.g. of the cooled clinker, in an other way than by simple heat exchange in the cement production line, e.g. for generating steam · CPC title

• C04B7/44 Primary

  Burning; Melting · CPC title

• F27B7/20

  Details, accessories or equipment specially adapted for rotary-drum furnaces · CPC title

• C04B7/43 Primary

  Heat treatment, e.g. precalcining, burning, melting; Cooling {(aspects only relating to the installation F27B)} · CPC title

• C04B2290/20

  Integrated combined plants or devices, e.g. combined foundry and concrete plant · CPC title